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    Chinese Journal of Catalysis
    2011, Vol. 32, No. 3
    Online: 04 March 2011

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    Knowledge on reaction mechanism can help to find kinetic resources for reducing catalyst deactivation. Potentialities were discussed by Prof. Petrov et al. (see pages 387–404). Theoretical analysis supported by experimental results evidenced: if product molecules induce generation of coke, the deactivation may be slower under diffusion control. An approach is suggested relating the availability of active sites of different configuration, adsorption properties, vulnerability, with deactivation and selectivity features of poly-functional catalysts.

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    Table of Contents
    Table of Contents for Vol.32 No. 3
    2011, 32 (3):  0-0. 
    Abstract ( 1290 )   PDF (1327KB) ( 756 )  
    Summary
    Reaction Mechanism and Deactivation Modes of Heterogeneous Catalytic Systems
    K. KUMBILIEVA1, L. PETROV2,*, Y. ALHAMED2, A. ALZAHRANI2
    2011, 32 (3):  387-404.  DOI: 10.1016/S1872-2067(10)60181-7
    Abstract ( 2535 )   [Full Text(HTML)] () PDF (449KB) ( 1841 )  
    Solving the problem of catalyst deactivation is essential in process design. To do this, various aspects of the kinetics of processes with catalyst deactivation, and their different mechanisms, are discussed. Catalyst deactivation often cannot be avoided, but more knowledge on its mechanism can help to find kinetic means to reduce its harmful consequences. When deactivation is caused by coke, the generation of coke precursors is the determining step in the deactivation kinetics. Different types of deactivation were distinguished that lead to different evolution of the process. The phenomenon of non-uniform coking can be linked to catalyst surface non-uniformity. For the class of catalysts with more than one type of active sites, an explanation was suggested for the observed trends in the deactivation modes. For catalytic processes using catalyst particles of industrial size, the influence of intraparticle diffusion resistance is important. The analysis showed that for a number of processes, the decrease of the reaction rate due to deactivation is less under diffusion control. For certain reaction mechanisms, there exist operation conditions where the rate of the process under diffusion control exceeds the rate in the kinetic control regime. A significant problem is the change of selectivity in the course of catalyst deactivation. The selectivity may either decrease or increase, and depends on the reaction mechanism during deactivation. The changes are larger when there is no diffusion resistance. The intentional poisoning of catalysts and its influence on catalyst activity and selectivity for the process of ethylene oxide production was discussed.
    Research papers
    Alkaline Earth Metal Modified NaY for Lactic Acid Dehydration to Acrylic Acid: Effect of Basic Sites on the Catalytic Performance
    YAN Jie1, YU Dinghua1,2, SUN Peng1, HUANG He1,2,*
    2011, 32 (3):  405-411.  DOI: 10.1016/S1872-2067(10)60188-X
    Abstract ( 3148 )   [Full Text(HTML)] () PDF (367KB) ( 1133 )  
    Various NaY zeolites modified by alkaline earth metals (Mg, Ca, Sr, and Ba) were synthesized and used as catalysts for the dehydration of lactic acid to acrylic acid to investigate the effects of cationic species on the structure and surface acid/base distribution of the NaY zeolites. The important factors that affect their catalytic performance were also identified. The catalysts were characterized by N2 physical adsorption/desorption, X-ray diffraction, temperature-programmed desorption of NH3, and temperature-programmed desorption of CO2. The results show that the basic sites that are induced by modified metallic species, particularly the medium basic sites, are mainly responsible for the formation of acrylic acid. The generation of acetaldehyde was affected by the acidic sites. Among the catalysts, 2%Ba/NaY showed the highest yield of acrylic acid at up to 44.6% (38% solution, LHSV = 3 h–1, 325 °C) because it contained the most medium basic sites and a suitable Ba2+ cluster character.
    Conversion of Methanol Using Modified H-MOR Zeolite Catalysts
    Sameh M. K. ABOUL-FOTOUH1,*, Noha A.K. ABOUL-GHEIT2, Marwa M. I. HASSAN1
    2011, 32 (3):  412-417.  DOI: 10.1016/S1872-2067(10)60187-8
    Abstract ( 2744 )   [Full Text(HTML)] () PDF (374KB) ( 1526 )  
    The conversion of methanol was carried out over various mordenite zeolite catalysts to evaluate their catalytic performance. A post-preparation treatment of the H-MOR catalyst by halogenation with NH4Cl or NH4F and by hydrohalogenation with HCl or HF was carried out and its effect on methanol conversion reactions at 100–300 °C in a continuous flow reactor was investigated. The as-synthesized H-mordenite (H-MOR) is generally more active during dimethyl ether (DME) production than the NH4-MOR and Na-MOR. Fluorinated treatment with HF or NH4F significantly improved the catalytic activity during methanol conversion and the formation of DME in comparison to chlorinated treatments with HCl or NH4Cl. This is principally attributed to the higher Si/Al ratio and an increase in the number of acid sites and their strength. Halogenation treatment with the acids of both F or Cl gave the highest conversion activity for DME production compared to halogenation treatments with the salts of the same halogens. Zeolite dealumination by the acids was more profound than that by the halogen ion salts, which resulted in a decrease in the crystallinity and crystallite sizes of the zeolite.
    Hydrothermal Stability of Meso-microporous Composites and Their Catalytic Cracking Performance
    HAN Wei, JIA Yuxin, XIONG Guoxing*, YANG Weishen*
    2011, 32 (3):  418-427.  DOI: 10.1016/S1872-2067(10)60177-5
    Abstract ( 2915 )   [Full Text(HTML)] () PDF (624KB) ( 1053 )  
    Meso-microporous composites show great promise for catalysis because of their variously-sized porous structures. A series of composites containing uniform mesopores and MFI zeolitic channels were prepared by a template-free sol-gel method. The composite containing silicalite-1 structures was found to be much more hydrothermally stable than MCM-41. The composites with ZSM-5 structures showed higher catalytic activity and resistance to deactivation than commercial HZSM-5 in the catalytic cracking reaction of 1,3,5-triisopropylbenzene. The conversion and catalytic cracking product distribution of 1,3,5-triisopropylbenzene depended highly on the mesopore size of the composites. Higher conversions and small molecule cracking products were obtained using composites with smaller mesopores.
    Nanostructured Maghemite-Supported Silver Catalysts for Styrene Epoxidation
    PAN Zhenyan1, HUA Li1, QIAO Yunxiang1, YANG Hanmin2, ZHAO Xiuge1, FENG Bo1, ZHU Wenwen1, HOU Zhenshan1,*
    2011, 32 (3):  428-435.  DOI: 10.1016/S1872-2067(10)60183-0
    Abstract ( 3223 )   [Full Text(HTML)] () PDF (682KB) ( 1141 )  
    The supported silver catalyst Ag/KOH-γ-Fe2O3 was prepared by simple impregnation and liquid reduction and then structurally characterized by X-ray diffraction, transmission electron microscopy, and X-ray photoelectron spectroscopy. The supported silver catalysts were highly efficient for the epoxidation of styrene using tert-butyl hydroperoxide as the oxidant and ethyl acetate as the reaction medium. The addition of KOH was found to increase the catalytic activity and selectivity significantly. Additionally, the magnetically recoverable γ-Fe2O3, as a support, allowed for an easy separation and recycling of the catalyst after the reaction.
    Highly Efficient Ru-Ba/AC Catalyst Promoted by Magnesium for Ammonia Synthesis
    NI Jun1, WANG Rong1,*, KONG Fanhua2, ZHANG Tianfu2, LIN Jianxin1, LIN bingyu1, WEI Kemei1
    2011, 32 (3):  436-439.  DOI: 10.1016/S1872-2067(10)60179-9
    Abstract ( 2857 )   [Full Text(HTML)] () PDF (431KB) ( 1104 )  
    The effect of alkaline-earth oxides as promoters on Ru/AC (AC = activated carbon) catalysts was explored. Alkaline-earth metal oxides can reduce the agglomeration of ruthenium particles at high temperatures, which increases the amount of available ruthenium. The influence of the Mg promoter on the distribution and activity of the Ru/AC catalyst were investigated by CO chemisorption, X-ray diffraction, and energy dispersive spectrometry and by an activity test for ammonia synthesis. The results show that a specific quantity of magnesium significantly promotes the uniform distribution of Ba and Ru on the surface of AC, which enhances catalytic activity. The introduction of Mg significantly improved the size of the Ru particles and increased the Ru surface area. The distribution and interaction were improved greatly for the Ba promoter and the Ru precursor on the surface of the AC because of the addition of the Mg promoter. The introduction of magnesium to Ru-Ba-K/AC significantly improved the utilization ratio of the noble metals and the performance-price ratio.
    Alkyl Sulfonate Functionalized Ionic Liquids: Synthesis, Properties, and Their Application in Esterification
    ZHAO Yingwei1,2, LI Zhen1,*, XIA Chungu1,*
    2011, 32 (3):  440-445.  DOI: 10.1016/S1872-2067(10)60178-7
    Abstract ( 3196 )   [Full Text(HTML)] () PDF (421KB) ( 1090 )  
    Ionic liquids based on alkyl sulfate anions and alkyl sulfonate functionalized cations were prepared from commercially available and cheap materials and their thermal-instability properties were studied in detail. These ionic liquids were active catalysts for esterification and they gave moderate to high yields. The catalytic performance was found to be much better than that of conventional non-cation functionalized ionic liquids and close to sulfonic acid functionalized ionic liquids. The catalytic process in this reaction was investigated by electrospray ionization mass spectrometry and a plausible reaction mechanism is suggested.
    Development of a Novel Conversion Equation as a Function of Catalytic Reaction Conditions in Tubular Reactors
    LI Qiaoling1, ZHANG Yuanhua1, CHEN Shiping1, FANG Weiping1,2,* and YANG Yiquan1,2,#
    2011, 32 (3):  446-450.  DOI: 10.1016/S1872-2067(10)60180-5
    Abstract ( 3847 )   [Full Text(HTML)] () PDF (420KB) ( 886 )  
    A comprehensive conversion equation was developed to simulate the catalytic reaction conditions (include temperature, pressure, residence time, and reaction composition) in tubular reactors: . This conversion equation is based on the characteristics of the power-exponential function  as well as the “variable reaction order” and “virtual reactant” concepts. Its validity was verified by fitting experiment data from three different catalytic systems such as the dehydrogenation of diethyl benzene, the hydrogenation of ethylbenzene, and the hydrodesulfurization of thiophene. The results show that the influences of reaction temperature, pressure, residence time, and reactant composition on the conversion of the reactant can be determined within a wide range of values. By comparison with the experimental data, the calculated conversions were all found to have a total average relative deviation of less than 2%. This suggests that the conversion equation is not limited to a specific catalyst system but could be suitable for various catalyst systems in tubular reactors.
    Vinyl Chloride Selectivity during Epoxidation on Oxygen Pre-adsorbed Ag(100): A Density-Functional Theory Study
    Lü Yongkang1,*, XI Ruixin1, REN Ruipeng1,2
    2011, 32 (3):  451-455.  DOI: 10.1016/S1872-2067(10)60197-0
    Abstract ( 2968 )   [Full Text(HTML)] () PDF (466KB) ( 1066 )  
    Vinyl chloride selectivity during epoxidation on an atomic oxygen pre-adsorbed Ag(100) surface using density functional theory (DFT) with the periodic slab model was investigated. The reaction mechanism is a two-step process where chloroethylene oxametallacycle intermediate (OMMC) is first formed and then converted to the products. Because of the asymmetry of vinyl chloride, two competitive reaction pathways are evident. The reaction energies and the activation energies of the processes were determined by the DFT calculations. Compared with the reaction activity energy, in one pathway the formation of chloroethylene epoxide (CE) is more favorable than the formation of chloroacetaldehyde (CA) whereas in the other pathway, the formation of CA is more favorable than the formation of CE and acetyl chloride. To further understand the reason for the selectivity difference in these different paths the projected density of states of the C atom and the Ag atom involved in the OMMC was calculated.
    Pre-reforming of Liquefied Petroleum Gas over Ni/CeO2/Al2O3 Catalyst under Low Molar Ratios of Steam to Carbon
    ZHAO Jingyue, ZOU Xiujing, WANG Xueguang*, LIU Hezhi, LI Lin, LU Xionggang, DING Weizhong*
    2011, 32 (3):  456-462.  DOI: 10.3724/SP.J.1088.2011.01034
    Abstract ( 3424 )   [Full Text(HTML)] () PDF (638KB) ( 1169 )  
    Ni/CeO2/Al2O3 catalyst samples with different Ni contents were prepared by co-impregnating boehmite with aqueous solution of cerium and nickel nitrates and characterized by X-ray diffraction, N2 adsorption, and temperature-programmed reduction. It was found that there was a strong interaction between Ni and CeO2 species. Addition of CeO2 promoted the reduction of NiAl2O4 to metal Ni, while nickel species in turn promoted the reduction of CeO2 and reacted with Al2O3 to CeAlO3. The pre-reforming of commercial liquefied petroleum gas (LPG) was investigated over Ni/CeO2/Al2O3 catalyst at low steam/carbon molar ratios (less than 1.0). The effects of Ni content, reaction temperature, and S/C molar ratio on the performance of the Ni/CeO2/Al2O3 catalyst were discussed. The results showed that the catalyst was highly active and stable for the steam reforming of LPG at 275–375 °C. Higher Ni content and S/C ratio promoted the steam reforming of LPG and substantially accelerated the methanation of COx and H2. The stability tests indicated that the Ni/CeO2/Al2O3 catalyst exhibited excellent stability and resistance to carbon deposition. The reaction mechanism for pre-reforming of higher hydrocarbons under lower S/C molar ratios was proposed.
    Baeyer-Villiger Oxidation of Cyclohexanone Catalyzed by SBA-15 Supported Silicotungstic Acid
    YANG Zhiwang, MA Zhenhong, NIU Lengyuan, MA Guofu, MA Hengchang, LEI Ziqiang*
    2011, 32 (3):  463-467.  DOI: 10.3724/SP.J.1088.2011.00928
    Abstract ( 3396 )   [Full Text(HTML)] () PDF (665KB) ( 1403 )  
    Silicotungstic acid (H4O40SiW12) was supported on SBA-15 with the content of 20% by impregnation. The structure and properties of the catalyst were characterized by Fourier transform infrared spectroscopy, X-ray diffraction, N2 adsorption-desorption, and transmission electron microscopy. H4O40SiW12 was highly dispersed on SBA-15 without structural change. The material was applied as an efficient catalyst for the Baeyer-Villiger oxidation of cyclohexanone under different conditions such as the catalyst amount, reaction temperature, and reaction time. When 10 mg of catalyst was used, the cyclohexanone conversion and selectivity for lactone were up to 86% and 99%, respectively, at 70 oC for 8 h. The catalyst had moderate reusability in the oxidation system.
    A Novel Thermoregulated-Acidic Ionic Liquid: Synthesis and Application as Catalyst in α-Pinene Hydration
    LIU Shiwei1, LI Lu1, YU Shitao1,*, XIE Congxia2, LIU Fusheng1, SONG Zhanqian1,3
    2011, 32 (3):  468-471.  DOI: 10.3724/SP.J.1088.2011.00930
    Abstract ( 2603 )   [Full Text(HTML)] () PDF (495KB) ( 975 )  
    A novel thermoregulated-acidic ionic liquid, 1-(3-sulfonic acid)-propyl-3-polyethylene glycol-yl imidazole dihydrogen phosphate ([PEOIM-SO3H]H2PO4), was synthesized, characterized, and used as a catalyst in the hydration of α-pinene. The ionic liquid had good thermoregulated and acidic catalytic performance in the hydration. Under the optimum conditions of n(α-pinene):n(chloroacetic):n(water) = 1:1:5, α-pinene 0.06 mol, ionic liquid 3.0 mmol, reaction temperature 80 oC, and reaction time 8 h, the α-pinene conversion was more than 89% and the terpineol selectivity was 65.0%. When the ionic liquid was reused for five times, the α-pinene conversion reached 85.8% and the terpineol selectivity was 66.8%.
    Cross-Coupling Reaction of Benzylic Halides with Allyltributylstannane Catalyzed by Cu(OTf)2
    YU Xiaoqiang1, MA Yongjie1, ZHAO Ziran2,*, XU Zhanwei1, BAO Ming1,*
    2011, 32 (3):  472-476.  DOI: 10.3724/SP.J.1088.2011.01018
    Abstract ( 3878 )   [Full Text(HTML)] () PDF (341KB) ( 1136 )  
    Cross-coupling reaction of benzylic halides with allyltributylstannane was investigated. Desired cross-coupling products were obtained in satisfactory yields using Cu(OTf)2 as the catalyst. For example, cross-coupling product 1-(but-3-en-1-yl)-4-phenylnaphthalene (3b) was obtained in 93% yield when the reaction of 1-chloromethyl-4-phenylnaphthalene with allyltributylstannane was carried out in the presence of 10 mol% of Cu(OTf)2 in CH2Cl2 at room temperature for 1 h. The reaction of a substrate bearing an electron-donating group on the aromatic ring was completed in a few minutes, whereas the reaction of a substrate having an electron-withdrawing group on the aromatic ring needed prolonged reaction time. 3b, 1-bromo-4-(but-3-en-1-yl)naphthalene (3c), and 1-(but-3-en-1-yl)-4-nitronaphthalene (3f) were unknown compounds and their structure was confirmed by 1H NMR, 13C NMR, IR, and HRMS.
    Preparation of Cr-Mn Mixed Oxide by Coprecipitation and Its Performance for Low-Temperature Selective Catalytic Reduction of NOx
    LI Xuehui*, LI Hua, GAO Xiang, CHEN Zhihang, YANG Qing, WANG Furong, WANG Lefu
    2011, 32 (3):  477-482.  DOI: 10.3724/SP.J.1088.2011.00832
    Abstract ( 3189 )   [Full Text(HTML)] () PDF (622KB) ( 1069 )  
    A series of Cr-Mn mixed-oxide catalysts comprising a novel CrMn1.5O4 crystal phase were prepared by the coprecipitation method and applied to low-temperature selective catalytic reduction (SCR) of NOx with NH3 in the presence of O2. The experimental results showed that the NOx conversion increased with the increase of Cr content and peaked at the Cr(0.4)-MnOx catalyst with the molar ratio of Cr/(Mn+Cr) = 0.4, which yielded nearly 90% NOx conversion at 140 oC with a high space velocity of 30 000 h-1. The characterization of N2 adsorption, X-ray diffraction, and X-ray photoelectron spectroscopy indicated that the addition of Cr generated the novel CrMn1.5O4 crystal phase and adjusted the surface electronic properties, leading to the enrichment of higher oxidation states Mn4+ and Mn3+ on the surface. This promotes the oxidation of NO and is helpful for the adsorption of NH3, so that the catalyst exhibits higher low-temperature SCR activity.
    Synchronous Synthesis and Immobilization of Pyridyl Porphyrins on Crosslinked Polystyrene Microspheres and Catalytic Oxidation Performance of Immobilized Cationic Co-Porphyrins
    TIAN Peng, GAO Baojiao*, CHEN Yingjun
    2011, 32 (3):  483-489.  DOI: 10.3724/SP.J.1088.2011.01030
    Abstract ( 2931 )   [Full Text(HTML)] () PDF (539KB) ( 1027 )  
     Pyridylaldehyde (PyAL) groups were bound onto the surface of crosslinked polystyrene (CPS) microspheres via quaternization between 4-pyridylaldehyde and chloromethyl groups of chloromethylated crosslinked polystyrene (CMCPS) microspheres, obtaining the modified microspheres PyAL-CPS. Subsequently, synchronous synthesis and immobilization of pyridylporphyrin on CPS microspheres were successfully realized using 4-pyridylaldehyde, pyrrole and the modified microspheres PyAL-CPS as the co-reactants via the Adler reaction between solid-liquid phases, resulting in functional microspheres PyP-CPS, on which pyridylporphyrin (PyP) was immobilized. The microspheres PyP-CPS were then allowed to react with methyl iodide, and PyP was transformed to N-methyl pyridyl porphyrin (MPyP) iodide, leading to the formation of MPyP-CPS microspheres, on which cationic porphyrin was immobilized. Finally, the solid catalyst CoMPyP-CPS, on which cationic cobalt porphyrin was immobilized, was prepared through the coordination reaction between MPyP-CPS microspheres and cobalt salt. The effects of the main factors on the synchronous synthesis and immobilization of pyridylporphyrin on CPS microspheres were examined, and the catalytic performance of the solid catalyst CoMPyP-CPS in the oxidation of ethylbenzene by molecular oxygen was investigated mainly. Besides, the catalytic character of the composite catalyst CPW, which was prepared by association of CoMPyP-CPS (C) and phospho-tungstic(PW)heteropoly acid, was also investigated. The results show that the synchronous synthesis and immobilization of pyridylporphyrin on CPS microspheres can be favourably carried out using PyAL-CPS microspheres, 4-pyridylaldehyde, and pyrrole in the solution as co-reactants via the Adler reaction between solid-liquid phases. The immobilized cationic cobaltporphyrin catalyst CoMPyP-CPS has excellent catalytic performance in the oxidation of ethylbenzene by molecular oxygen, and the composite catalyst CPW possesses much higher catalytic activity.
    Catalytic Properties of α-Diimine-Ni (II) Catalyst Containing Electron Withdrawing Substituent for Ethylene Polymerization
    YUAN Jianchao*, WANG Xuehu, LIU Yufeng, MEI Tongjian
    2011, 32 (3):  490-494.  DOI: 10.3724/SP.J.1088.2011.01040
    Abstract ( 3385 )   [Full Text(HTML)] () PDF (550KB) ( 913 )  
    A new Br-substituted α-diimine ligand and its corresponding Ni(II) complex, {bis[N,N′-(4-bromo-2, 6-dimethylphenyl)imino] acenaphthene}dibromonicke (2) were successfully synthesized and characterized by 1H and 13C nuclear magnetic resonance, elemental analysis, Fourier transform infrared spectroscopy and X-ray photoelectron spectroscopy. The catalytic system, complex 2/diethylaluminium chloride (DEAC) showed higher activity for ethylene polymerization. The highest activity (3.73 × 107 g/(mol.h.MPa)) was obtained with the Al/Ni molar ratio of 600 at 25 ºC. The catalyst containing electron-withdrawing group Br showed better thermodynamic stability and almost the same catalytic activity compared with the Br-free catalyst. Branching degree was increased in the presence of electron-withdrawing group Br.
    Effects of Ru and Cu Promoters on Fischer-Tropsch Synthesis over Fe-Based Catalysts
    WANG Lili1,2, WU Baoshan1,*, LI Yongwang1
    2011, 32 (3):  495-501.  DOI: 10.3724/SP.J.1088.2011.01128
    Abstract ( 2915 )   [Full Text(HTML)] () PDF (681KB) ( 932 )  
    The effects of Ru and Cu promoters on the textural properties, phase composition, reduction and carburization behavior, and catalytic performance of Fe-based Fischer-Tropsch synthesis (FTS) catalysts without K promoter were investigated. The catalysts were characterized by N2 physical adsorption, X-ray diffraction, H2 and CO temperature-programmed reduction, Mössbauer effect spectroscopy. The FTS performance of the catalysts was tested in a fixed-bed reactor under the conditions of n(H2)/n(CO) = 2.0, t = 260 oC, p = 1.5 MPa and GHSV = 2000 h-1. The results indicated that both Ru and Cu enhance the dispersion of iron oxides and facilitate the reduction and carburization of the catalysts, which was more obvious for the Cu promoter. Ru and Cu both increase the activity of the catalysts to some extent. Besides, the Cu promoter increased the C5+ selectivity and hindered the CH4 formation while Ru exhibited the opposite trend.
    Effects of BaO Content on Properties of Ba-Modified Alumina and Catalytic Performance of Its Supported Pt-Rh Close-Coupled Catalysts
    YAO Yanling, HE Shengnan, SHI Zhonghua, GONG Maochu, CHEN Yaoqiang*
    2011, 32 (3):  502-507.  DOI: 10.3724/SP.J.1088.2011.01122
    Abstract ( 3077 )   [Full Text(HTML)] () PDF (592KB) ( 906 )  
    In order to improve catalytic activity and thermal resistance of close-coupled catalysts, Ba-modified alumina (Ba-Al2O3) with different BaO contents was prepared by peptization method. All samples were characterized by low temperature N2 adsorption-desorption, X-ray diffraction, and NH3 temperature-programmed desorption. The results showed that the Ba-Al2O3 sample with 8% BaO exhibited the best textural properties, the largest acidic amount, and the strongest surface acidity. Its specific surface area and pore volume were 142 m2/g and 0.45 ml/g after calcination at 1273 K for 5 h and 114 m2/g and 0.37 ml/g after calcination at 1373 K for 5 h, respectively. Pt-Rh close-coupled catalysts supported on Ba-Al2O3 were prepared by impregnation method with Pt-Rh content of 1.5 g/L. The catalytic activity results showed that adding BaO into the support can effectively improve the catalytst activity in propane conversion. When the BaO content was 8%, the catalyst exhibited the best catalytic performance. The light-off temperatures for propane over fresh and aged catalysts were 513 and 557 K, respectively.
    Preparation of Nitrogen-Modified Titania with Urea as Nitrogen Source and Its Modification Mechanism
    HUANG Tao, ZHANG Guoliang*, WANG Ling, LIU Liangjun, SUN Xiping
    2011, 32 (3):  508-512.  DOI: 10.3724/SP.J.1088.2011.01121
    Abstract ( 3496 )   [Full Text(HTML)] () PDF (523KB) ( 1265 )  
    A nitrogen-modified TiO2 (N-TiO2) catalyst with different nitrogen content was prepared by a modified sol-gel method, using tetrabutyl titanate as the precursor and urea as the nitrogen source. The catalyst samples were used in the photocatalytic reduction of Cr(Ⅵ) under visible light, using formic acid as a hole scavenger to enhance the photocatalytic reduction reaction. The results demonstrated that the N-TiO2 catalyst had higher photocatalytic activity than bare TiO2, and the N-TiO2 sample with 10% (molar ratio) nitrogen calcined at 400 oC held the highest photocatalytic efficiency. The N-TiO2 samples were characterized by X-ray diffraction, X-ray photoelectron spectroscopy, Fourier transform infrared spectroscopy, and ultraviolet visible diffuse reflectance spectroscopy. The results showed that the higher photocatalytic activity of the N-TiO2 sample calcined at 400 oC was mostly attributed to the melon condensation products, which acted as visible-light sensitizers.
    Selective Hydrogenation of Crotonaldehyde over Pt/Ce0.8La0.2O1.9 Catalysts
    CHEN Ping, XIE Guanqun, ZHENG Haiying, ZHU Lin, LUO Mengfei*
    2011, 32 (3):  513-519.  DOI: 10.3724/SP.J.1088.2011.01124
    Abstract ( 3178 )   [Full Text(HTML)] () PDF (640KB) ( 920 )  
    The vapor-phase selective hydrogenation of crotonaldehyde was carried out over Pt/Ce0.8La0.2O1.9 catalysts prepared by impregnation. The catalysts were characterized by X-ray powder diffraction, temperature-programmed reduction, NH3 temperature- programmed desorption, and Raman spectroscopy. It was found that with increasing Pt loading in Pt/Ce0.8La0.2O1.9, both the activity (TOF) and selectivity for crotyl alcohol increased first and then decreased a little. The 3%Pt/Ce0.8La0.2O1.9 catalyst showed the highest activity (TOF) and selectivity for crotyl alcohol in hydrogenation of crotonaldehyde (4.01 × 10-3 s-1 and 53.6%, respectively). It was concluded that the catalytic performance of the catalysts depends on the surface acidity and the Pt particle size. Carbon deposition formed on the catalyst surface during the hydrogenaton process may account for the decrease in the catalytic activity and selectivity for crotyl alcohol.